Classifications

• • C—CHEMISTRY; METALLURGY
  • C06—EXPLOSIVES; MATCHES
  • C06B—EXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
  • C06B21/00—Apparatus or methods for working-up explosives, e.g. forming, cutting, drying
  • C06B21/0033—Shaping the mixture
  • C06B21/0066—Shaping the mixture by granulation, e.g. flaking

Definitions

• hard black powder is generally used as prepared in a generally used process comprising the following steps:
• the powder must per se burn at a constant rate
• the powder must be able to be fed evenly to the fuscord.
• the raw materials In order to fulfil requirement (1), the raw materials must be crushed down to a high degree of fineness, at least 90% finer than 15 microns. Such a meal black powder can hardly and perhaps not at all be fed evenly into the fuse. In other words, these two conditions are not readily compatible with a simple meal black powder, and this is the reason for the varying burning-times which often occur.
• the method comprises: One starts with a suitable meal black powder of sufficient fineness (at least 90% finer than 15 microns) and of a suitable composition, e.g.:
• the meal black powder is prepared in any known way, such as, e.g., by means of ball mills, jet mills, wheel mills or in other ways.
• a suitable amount of water such as, e.g., about 20 %, in a suitable blending apparatus.
• the moist powder is compressed lightly, for instance between two belts, between belts and rollers, between two rollers or in a hydraulic press.
• the compressing shall be strong enough for the powder to form a coherent body after compressing.
• the powder is then rubbed through a sieve having a suitable mesh size, e.g., 0.5 mm and is thereafter passed into a rotating, circular container in which the powder agglomerates to spherical grains.
• the agglomeration is continued until the grains have achieved a size of maximum 1 mm. This takes place during about 5 minutes.
• the powder grains are then passed into a suitable drying device, preferably of the fluidized bed type, wherein the moisture is reduced from 20 % to about 1 % by means of hot (70°C.), dry air. After the drying process the powder is sifted so that the grain size of the accepted powder lies between 1.0 mm and 0.3 mm.
• the finer and coarser fractions are returned to the raw material mills and are reground with the raw materials.
• This method is particularly well suited for continuous and automatic operations. This is of great importance as seen from a safety point of view because by automatic operations it is no longer necessary for the operators to be present in the danger zone during the powder production, and in continuous processes the amounts of explosives being momentarily produced will at any time be significantly less than in discontinuous production processes.
• the meal black powder In continuous and automatic production it is highly suitable to prepare the meal black powder according to Norwegian Pat. No. 118,356.
• the meal black powder will then fall into the blending or kneading apparatus in which the water is added at the same time as the powder is transported through the apparatus, and the moist powder falls out and directly into the rolling mill.
• the sieving device is located underneath the rolling mill. It is equipped with a rotating brush which brushes the powder through the sieve. Underneath the sieving device the rotating agglomeration cylinder is located. It is obliquely arranged so that the powder moves therethrough at the same time as it is rolled and agglomerated to spherical grains.
• the drying apparatus is located underneath the agglomeration cylinder and while being dried the powder is moved through the dryer.
• the sieving device is located. It is equipped with two sieving cloths to that the fraction of accepted size is drawn off in the centre. The fractions which are too coarse and too fine are combined and transported continuously back to the mill by means of a vibration transporter.
• the powder has a high degree of moisture (about 20 % of water), which makes it substantially not ignitious, and at least very hardly ignitious relative to conventional black powder having a moisture content of maximum 5 %.
• the production capacity is much greater than in a conventional plant of the same size.

Landscapes

• Chemical & Material Sciences (AREA)
• Organic Chemistry (AREA)
• Solid Fuels And Fuel-Associated Substances (AREA)
• Disintegrating Or Milling (AREA)
• Fodder In General (AREA)
• Confectionery (AREA)
• Coloring Foods And Improving Nutritive Qualities (AREA)

Applications Claiming Priority (2)

Publications (1)

Family

ID=19881569

Family Applications (1)

Country Status (6)

Cited By (6)

Families Citing this family (1)

Citations (1)

• 1974
  • 1974-04-22 NO NO741437A patent/NO132988C/no unknown
• 1975
  • 1975-04-21 ZA ZA00752562A patent/ZA752562B/xx unknown
  • 1975-04-21 CA CA225,096A patent/CA1066511A/en not_active Expired
  • 1975-04-21 US US05/569,681 patent/US3980741A/en not_active Expired - Lifetime
  • 1975-04-22 GB GB16551/75A patent/GB1496433A/en not_active Expired
  • 1975-04-22 DE DE19752517670 patent/DE2517670A1/de not_active Withdrawn

Patent Citations (1)

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